Dry fluff pulp sheet additive

ABSTRACT

A process is provided for making a fluff pulp sheet, comprising forming a web comprising fluff pulp fibers; and applying at least one debonder surfactant to the web, to make the fluff pulp sheet. A fluff pulp sheet is also provided, comprising a web comprising fluff pulp fibers; at least one debonder surfactant; and a fiberization energy of &lt;145 kJ/kg. Products and uses of the fluff pulp sheet are also provided.

BACKGROUND Field of the Invention

The invention relates to fluff pulp sheets, processes for making, andtheir use.

BRIEF DESCRIPTION OF THE FIGURES

Various embodiments are described in conjunction with the accompanyingfigures, in which:

FIG. 1 shows a schematic example of one embodiment of a suitablepapermaking machine, wherein A is a head box; B is a composition (e.g.,comprising fluff pulp fibers) applied to a table C from head box B; D isa formation shower; E is a suction box; F is a first press; G is asecond press or transition to dryer H; I is a formation shower; J is areel for taking up the finished fluff pulp sheet K; and L is an arrowshowing the machine direction of the product as it progresses from headbox A to reel J.

DETAILED DESCRIPTION OF THE SEVERAL EMBODIMENTS

One embodiment of the subject matter claimed herein results insignificantly reduced operational risk, e.g., sheet breaking, in themanufacture of fluff pulp sheets. Another embodiment of the subjectmatter claimed herein results in improved fluff shred quality of fluffpulp sheets. Another embodiment of the subject matter claimed hereinresults in improved fluff fiber singulation of fluff pulp sheets.Another embodiment of the subject matter claimed herein results inreduced fiberization energy of fluff pulp sheets. Another embodiment ofthe subject matter claimed herein results in good Mullen values of fluffpulp sheets. Another embodiment of the subject matter claimed hereinresults in a fluff pulp sheet with reduced fiberization energy but whichmaintains good Mullen value. Another embodiment of the subject matterclaimed herein is a fluff pulp sheet having improved surfactantretention. Another embodiment of the subject matter claimed herein is afluff pulp sheet or absorbent product obtained therefrom having improvedabsorbency and low absorption times. In one embodiment, the fluff pulpsheet can be processed at high speeds without sheet breaks or otherprocessing issues. In another embodiment, the subject matter claimedherein avoids the disadvantages of conveying a mechanically weak sheetthrough a paper machine.

One embodiment of the invention relates to a process for making a fluffpulp sheet, comprising:

forming a web comprising fluff pulp fibers; and

applying at least one debonder surfactant to the web, to make the fluffpulp sheet.

In one embodiment, the forming comprises one or more of contacting afluff pulp mixture comprising fluff pulp fibers and water with a tablein a papermaking machine, removing at least a portion of water from afluff pulp mixture comprising fluff pulp fibers and water with a suctionbox under a table in a papermaking machine, at least partially drying afluff pulp mixture comprising fluff pulp fibers and water in a flotationdryer, heating a fluff pulp mixture comprising fluff pulp fibers andwater, heating the debonder surfactant, or a combination thereof.

The debonder surfactant may be suitably applied to the web. For example,the debonder surfactant may be suitably sprayed onto the web using aformation shower or spray boom over the table, coated onto the web usingknown coating methods in the papermaking arts, or the web may beimmersed into the debonder surfactant. Combinations of applicationmethods are possible.

In one embodiment, the debonder surfactant is sprayed onto the web.

In one embodiment, the spraying is carried out using one or moreformation showers over a table in a papermaking machine.

In embodiment, the web may be dried in a dryer, to form a dried web orfluff pulp sheet. The web may be suitably dried in a drying section. Anymethod for drying commonly known in the art of fluff pulp papermakingmay be utilized. The drying section may include and contain a dryingcan, flotation dryer, cylinder drying, Condebelt drying, IR, or otherdrying means and mechanisms known in the art. The fluff pulp sheet maybe dried so as to contain any selected amount of water. In oneembodiment, the web is dried using a flotation dryer.

In one embodiment, the applying comprises applying the debondersurfactant to the dried web.

In another embodiment, a debonder surfactant may further and optionallybe applied to the fluff pulp sheet. The thus-applied second debondersurfactant may be the same or different from the debonder surfactantapplied to the web. In one embodiment, the second debonder surfactant isapplied to the fluff pulp sheet after the last drying step. In oneembodiment the second debonder surfactant is applied to the fluff pulpsheet before the sheet is taken up on the reel. The second debondersurfactant may be suitably applied by spraying, for example, from asecond formation shower or spray boom located at the dry end.

The web may be suitably dried to a moisture content of between 0 and70%. This range includes all values and subranges therebetween,including 0, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5,6, 7, 8, 9, 10, 12, 14, 16, 18, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65,70% or any combination thereof or range therein. In one embodiment, theweb is dried to a moisture content of ≤70%. In another embodiment, theweb is dried to a moisture content of ≤50%. In another embodiment, theweb is dried to a moisture content of ≤25%. In another embodiment, theweb is dried to a moisture content of ≤10%. In another embodiment, theweb is dried to a moisture content of ≤7%. In another embodiment, theweb is dried to a moisture content of about 6.3%.

In one embodiment, the web may have a basis weight ranging from 100 to1100 gsm. This range includes all values and subranges therein, forexample 100, 125, 150, 175, 200, 225, 250, 275, 300, 400, 500, 600, 700,800, 900, 1000, 1100, or any combination thereof or range therein.

In one embodiment, the solids content of the web and/or fluff pulp sheetat the point or points of applying the debonder surfactant may suitablyrange from 1 to 100%. This range includes all values and subrangestherebetween, including 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30,35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 99, 100%, or anycombination thereof or any range therein. In one embodiment, the solidscontent of the web and/or fluff pulp sheet at the point or points ofapplying one or more debonder surfactant is >1%. In another embodiment,the solids content of the web and/or fluff pulp sheet at the point orpoints of applying one or more debonder surfactant is >25%. In anotherembodiment, the solids content of the web and/or fluff pulp sheet at thepoint or points of applying one or more debonder surfactant is >50%.

In one embodiment, the fluff pulp mixture further comprises one or moreadditive such as whitener, colorant, pigment, optical brightening agent,wetting agent, binder, bleaching agent, other additive, or a combinationthereof. If present, the amount of additive is not particularly limited.In one embodiment, the additive may be present in amounts ranging fromabout 0.005 to about 50 weight percent based on the weight of the fluffpulp mixture. This range includes all values and subranges therebetween,including about 0.005, 0.006, 0.007, 0.008, 0.009, 0.01, 0.02, 0.03,0.04, 0.05, 0.06, 0.07, 0.08, 0.09, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30, 35, 40, 45, and50 weight percent, or any combination thereof, based on the weight ofthe fluff pulp mixture.

In one embodiment, the web comprises a solids content of >1% by weight.This range includes all values and subranges therein, including 100, 99,98, 97, 96, 95, 94, 93, 92, 91, 90, 85, 80, 75, 70, 65, 60, 55, 50, 45,40, 35, 30, 25, 20, 15, 10, 9, 8, 7, 6, 5, 4, 3, 2, >1%, or anycombination thereof or range therein.

In one embodiment, the debonder surfactant is applied neat or aspurchased. In another embodiment, the debonder surfactant is used incombination with one or more second debonder surfactant. In anotherembodiment, the debonder surfactant is applied from a solution,dispersion, emulsion, or the like. If applied in solution, dispersion,emulsion, or the like, or combination thereof. In one embodiment, ifapplied in solution, dispersion, emulsion, or the like, the debondersurfactant concentration may suitably range from 1 to 50% by weightsolids content of debonder surfactant to the weight of solution,dispersion, emulsion, or the like. This range includes all values andsubranges therebetween, including 0.5, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10,11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 25, 30, 35, 40, 45, 50%, or anycombination thereof or range therein.

In one embodiment, the debonder surfactant is in the form of acomposition further comprising water and optionally one or more pHadjusting agent, whitener, colorant, pigment, optical brightening agent,wetting agent, binder, bleaching agent, trivalent cationic metal, alum,other additive, or a combination thereof. If present, the amount ofadditive is not particularly limited. In one embodiment, the additivemay be present in amounts ranging from about 0.005 to about 50 weightpercent based on the weight of the debonder surfactant composition. Thisrange includes all values and subranges therebetween, including about0.005, 0.006, 0.007, 0.008, 0.009, 0.01, 0.02, 0.03, 0.04, 0.05, 0.06,0.07, 0.08, 0.09, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3,4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30, 35, 40, 45, and 50 weight percent,or any combination thereof, based on the weight of the debondersurfactant composition.

Debonder surfactants are known in the fluff pulp and fluff pulp fiberarts. Any debonder surfactant is suitable for use in the presentapplication, and the selection thereof is within the skill of oneknowledgeable in the fluff pulp and fluff pulp fiber arts. Someexamples, which are not intended to be limiting, include linear orbranched monoalkyl amine, linear or branched dialkyl amine, linear orbranched tertiary alkyl amine, linear or branched quaternary alkylamine, ethoxylated alcohol, linear or branched, saturated or unsaturatedhydrocarbon surfactant, fatty acid amide, fatty acid amide quaternaryammonium salt, dialkyl dimethyl quaternary ammonium salt,dialkylimidazolinium quaternary ammonium salt, dialkyl ester quaternaryammonium salt, triethanolamine-ditallow fatty acid, fatty acid ester ofethoxylated primary amine, ethoxylated quaternary ammonium salt, dialkylamide of fatty acid, dialkyl amide of fatty acid, cationic surfactant,non-ionic surfactant, C₁₆-C₁₈ unsaturated alkyl alcohol ethoxylate,commercially available compound having CAS Registry No. 68155-01-1,commercially available compound having CAS Registry No. 26316-40-5,commercially available F60™, commercially available Cartaflex TS LIQ™,commercially available F639™, commercially available Hercules PS9456™,commercially available Cellulose Solutions 840™, commercially availableCellulose Solutions 1009™, commercially available EKA 509H™,commercially available EKA 639™, alone, or in any combination. Otherexamples of debonder surfactants are disclosed in U.S. Pat. No.4,425,186, the contents of which being hereby incorporated by reference.

Given the teachings herein, and the knowledge of one skilled in thefluff pulp papermaking arts, one can easily determine the method ofapplying the debonder surfactant to the web, and the amount,composition, temperature, residence time, and the like, to carry out thesubject matter claimed herein. For example, the total amount of debondersurfactant in the web and/or in the finished fluff pulp sheet may beincreased or decreased or otherwise controlled by controlling thevarious points of addition. For example, the amount of debondersurfactant applied at the wet end may be increased or decreased byrespectively decreasing or increasing that amount applied at the dryend. Further one or more than one of the same or different type ofdebonder surfactant, or any combination thereof, may be applied at anypoint in the process.

In another embodiment, the web further comprises water and optionallyone or more debonder surfactant, pH adjusting agent, whitener, colorant,pigment, optical brightening agent, wetting agent, binder, bleachingagent, trivalent cationic metal, alum, other additive, or a combinationthereof.

In one embodiment, the finished fluff pulp sheet may be fiberized orshredded, in accordance with methods known in the art. For example, thefiberizing or shredding may be carried out in a hammermill.

In one embodiment, the fluff pulp sheet and/or fiberized or shreddedfluff pulp sheet, or a combination thereof may be suitably incorporatedinto one or more of an adsorbent product, paper product, personal careproduct, medical product, insulating product, construction product,structural material, cement, food product, veterinary product, packagingproduct, diaper, tampon, sanitary napkin, gauze, bandage, fireretardant, or a combination thereof. These products and methods fortheir manufacture and use are well known to those of ordinary skill inthe art.

Another embodiment relates to a fluff pulp sheet, made by the processdescribed herein.

Another embodiment relates to a fluff pulp sheet, comprising:

a web comprising fluff pulp fibers;

at least one debonder surfactant; and

a fiberization energy of <145 kJ/kg.

The fiberization energy, sometimes called the shred energy, of the fluffpulp sheet is suitably less than 145 kJ/kg. This range includes allvalues and subranges therebetween, including 1, 2, 3, 4, 5, 6, 7, 8, 9,10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95,100, 105, 110, 115, 120, 125, 130, 135, 140, 145 kJ/kg, or anycombination thereof or any range therein. In one embodiment, thefiberization energy of the fluff pulp sheet is less than 135 kJ/kg. Inanother embodiment, the fiberization energy of the fluff pulp sheet isfrom 120 to less than 145 kJ/kg. In another embodiment, the fiberizationenergy of the fluff pulp sheet is less than 120 kJ/kg. In anotherembodiment, the fiberization energy of the fluff pulp sheet is from 100to 120 kJ/kg. In another embodiment, the fiberization energy of thefluff pulp sheet is less than 100 kJ/kg. In another embodiment, thefiberization energy of the fluff pulp sheet is less than 95 kJ/kg.

In one embodiment, the fluff pulp sheet has a SCAN-C 33:80 adsorptiontime of <4.0 s. This range includes all values and subrangestherebetween, including 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9,2, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3, 3.0, 3.1, 3.2,3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, <4.0 s, or any range therein.

In one embodiment, the fluff pulp sheet on screen fractionation has a %Good of ≥50%. This range includes all values and subranges therebetween,including 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100%, or any rangetherein.

In one embodiment, the fluff pulp sheet on screen fractionation has a %Fines of ≤40%. This range includes all values and subrangestherebetween, including 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30,35, 40%, or any combination thereof or any range therein.

In one embodiment, the fluff pulp sheet on screen fractionation has a %Pieces of ≤30%. This range includes all values and subrangestherebetween, including 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30%,or any combination thereof or any range therein.

In one embodiment, the fluff pulp sheet has a Mullen of ≥90 psi. Thisrange includes all values and subranges therebetween, including 90, 95,100, 105, 110, 115, 120, 125, 130, 135, 140, 145, 150, 155, 160, 165,170, 175, 180, 185, 190, 195, 200, 205, 210, 215, 220, 225, 230, 235,240, 245, 250 psi, and higher, or any range therein.

In one embodiment, the fluff pulp sheet contains the debonder surfactantin an amount of ≥1 lb solids debonder surfactant per ton of the fluffpulp fibers. This range includes all values and subranges therebetween,including 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2, 2.0, 2.1,2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5,3.6, 3.7, 3.8, 3.9, 4, 4.0, 5, 5.0, 6, 7, 8, 9, 10, 15, 20 lb solidsdebonder surfactant per ton of the fluff pulp fibers, and higher, or anycombination thereof or any range therein. In one embodiment, if morethan one debonder surfactant is used, this range is the total amountover all the debonder surfactants present in the fluff pulp sheet.

In one embodiment, the fluff pulp sheet has a moisture content of 25% orless. This range includes all values and subranges therebetween,including 0, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5,6, 7, 8, 9, 10, 12, 14, 16, 18, 20, 25%, or any combination thereof orrange therein. In another embodiment, the fluff pulp sheet has amoisture content of 20% or less. In another embodiment, the fluff pulpsheet has a moisture content of 10% or less. In another embodiment, thefluff pulp sheet has a moisture content of 7% or less. In anotherembodiment, the fluff pulp sheet has a moisture content of about 6.3%.

In one embodiment, the fluff pulp sheet has a density of 0.5 to 0.75g/cc. This range includes all values and subranges therebetween,including 0.5, 0.55, 0.6, 0.65, 0.7, and 0.75 g/cc, or any rangetherein.

In one embodiment, the fluff pulp sheet has a caliper of 40 to 70 mm.This range includes all values and subranges therebetween, including 40,45, 50, 55, 60, 65, 70 mm, and any range therein.

In one embodiment, the fluff pulp sheet may have a basis weight rangingfrom 100 to 1100 gsm. This range includes all values and subrangestherein, for example 100, 125, 150, 175, 200, 225, 250, 275, 300, 400,500, 600, 700, 800, 900, 1000, 1100, or any combination thereof or rangetherein.

Another embodiment relates to an adsorbent product, paper product,personal care product, medical product, insulating product, constructionproduct, structural material, cement, food product, veterinary product,packaging product, diaper, tampon, sanitary napkin, gauze, bandage, fireretardant, or a combination thereof, comprising the fluff pulp sheetand/or fiberized or shredded fluff pulp sheet, or a combination thereof.

Another embodiment relates to the use of an adsorbent product, paperproduct, personal care product, medical product, insulating product,construction product, structural material, cement, food product,veterinary product, packaging product, diaper, tampon, sanitary napkin,gauze, bandage, fire retardant, or a combination thereof, comprising thefluff pulp sheet and/or fiberized or shredded fluff pulp sheet, or acombination thereof.

Fluff pulp and fluff pulp fibers are known in the papermaking art. Anyfluff pulp or fluff pulp fiber is suitable for use in the presentapplication, and the selection thereof is within the skill of oneknowledgeable in the fluff pulp and fluff pulp fiber arts. One or morethan one, or any combination thereof, of fluff pulp and/or fluff pulpfibers may be used. The fluff pulp and fluff pulp fibers may be treatedor untreated, and they may optionally contain one or more than oneadditives, or combination thereof, which are known in the art. Given theteachings herein, the level of treatment, if desired, and the amount ofadditives may be readily determined by one of ordinary skill in thefluff pulp and fluff pulp fiber arts.

Similarly, the formation of a web of fluff pulp or fluff pulp fibers orfrom a fluff pulp mixture or furnish onto a table from a headbox in apapermaking machine is within the skill of one knowledgeable in thefluff pulp and fluff pulp fiber arts.

The type of fluff pulp or fluff pulp fiber suitable for use herein isnot intended to be limiting. Fluff pulp typically includes cellulosicfiber. The type of cellulosic fiber is not critical, and any such fiberknown or suitable for use in fluff pulp paper can be used. For example,the fluff pulp can made from pulp fibers derived from hardwood trees,softwood trees, or a combination of hardwood and softwood trees. Thefluff pulp fibers may be prepared by one or more known or suitabledigestion, refining, and/or bleaching operations such as, for example,known mechanical, thermomechanical, chemical and/or semichemical pulpingand/or other well known pulping processes. The term, “hardwood pulps” asmay be used herein include fibrous pulp derived from the woody substanceof deciduous trees (angiosperms) such as birch, oak, beech, maple, andeucalyptus. The term, “softwood pulps” as may be used herein includefibrous pulps derived from the woody substance of coniferous trees(gymnosperms) such as varieties of fir, spruce, and pine, as for exampleloblolly pine, slash pine, Colorado spruce, balsam fir and Douglas fir.In some embodiments, at least a portion of the pulp fibers may beprovided from non-woody herbaceous plants including, but not limited to,kenaf, hemp, jute, flax, sisal, or abaca, although legal restrictionsand other considerations may make the utilization of hemp and otherfiber sources impractical or impossible. Either bleached or unbleachedfluff pulp fiber may be utilized. Recycled fluff pulp fibers are alsosuitable for use.

The fluff pulp sheet may suitably contain from 1 to 99 wt % of fluffpulp fibers based upon the total weight of the fluff pulp sheet. In oneembodiment, the fluff pulp sheet may contain from 5 to 95 wt % of fluffpulp fibers based upon the total weight of the fluff pulp sheet. Theseranges include any and all values and subranges therebetween, forexample, 1, 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75,80, 85, 90, 95 and 99 wt %.

The fluff pulp sheet may optionally contain from 1 to 100 wt % fluffpulp fibers originating from softwood species based upon the totalamount of fluff pulp fibers in the fluff pulp sheet. In one embodiment,the fluff pulp sheet may contain 10 to 60 wt % fluff pulp fibersoriginating from softwood species based upon the total amount of fluffpulp fibers in the fluff pulp sheet. These ranges include 1, 2, 5, 10,15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, and100 wt % and any and all ranges and subranges therein, based upon thetotal amount of fluff pulp fibers in the fluff pulp sheet.

All or part of the softwood fibers may optionally originate fromsoftwood species having a Canadian Standard Freeness (CSF) of from 300to 750. In one embodiment, the fluff pulp sheet contains fluff pulpfibers from a softwood species having a CSF from 400 to 550. Theseranges include any and all values and subranges therebetween, forexample, 300, 310, 320, 330, 340, 350, 360, 370, 380, 390, 400, 410,420, 430, 440, 450, 460, 470, 480, 490, 500, 510, 520, 530, 540, 550,560, 570, 580, 590, 600, 610, 620, 630, 640, 650, 660, 670, 680, 690,700, 710, 720, 730, 740, and 750 CSF. Canadian Standard Freeness is asmeasured by TAPPI T-227 standard test.

The fluff pulp sheet may optionally contain from 1 to 100 wt % fluffpulp fibers originating from hardwood species based upon the totalamount of fluff pulp fibers in the fluff pulp sheet. In one embodiment,the fluff pulp sheet may contain from 30 to 90 wt % fluff pulp fibersoriginating from hardwood species, based upon the total amount of fluffpulp fibers in the fluff pulp sheet. These ranges include 1, 2, 5, 10,15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, and100 wt %, and any and all values and subranges therein, based upon thetotal amount of fluff pulp fibers in the fluff pulp sheet.

All or part of the hardwood fibers may optionally originate fromhardwood species having a Canadian Standard Freeness of from 300 to 750.In one embodiment, the fluff pulp sheet may contain fibers from hardwoodspecies having CSF values of from 400 to 550. These ranges include 300,310, 320, 330, 340, 350, 360, 370, 380, 390, 400, 410, 420, 430, 440,450, 460, 470, 480, 490, 500, 510, 520, 530, 540, 550, 560, 570, 580,590, 600, 610, 620, 630, 640, 650, 660, 670, 680, 690, 700, 710, 720,730, 740, and 750 CSF, and any and all ranges and subranges therein.

The fluff pulp sheet may optionally contain less refined fluff pulpfibers, for example, less refined softwood fibers, less refinedhardwood, or both. Combinations of less refined and more refined fibersare possible. In one embodiment, the fluff pulp sheet contains fibersthat are at least 2% less refined than that of fluff pulp fibers used inconventional fluff pulp sheets. This range includes all values andsubranges therebetween, including at least 2, 5, 10, 15, and 20%. Forexample, if a conventional fluff pulp sheet contains fibers, softwoodand/or hardwood, having a Canadian Standard Freeness of 350, then, inone embodiment, the fluff pulp sheet may contain fibers having a CSF of385 (i.e. refined 10% less than conventional).

When the fluff pulp sheet contains both hardwood fluff pulp fibers andsoftwood fluff pulp fibers, the hardwood/softwood fluff pulp fiberweight ratio may optionally range from 0.001 to 1000. In one embodiment,the hardwood/softwood ratio may range from 90/10 to 30/60. These rangesinclude all values and subranges therebetween, including 0.001, 0.002,0.005, 0.01, 0.02, 0.05, 0.1, 0.2, 0.5, 1, 2, 5, 10, 15, 20, 25, 30, 35,40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 200, 300, 400, 500,600, 700, 800, 900, and 1000.

The softwood fibers, hardwood fibers, or both may be optionally modifiedby physical and/or chemical processes to obtain the fluff pulp. Examplesof physical processes include, but are not limited to, electromagneticand mechanical processes. Examples of electrical modifications include,but are not limited to, processes involving contacting the fibers withan electromagnetic energy source such as light and/or electricalcurrent. Examples of mechanical modifications include, but are notlimited to, processes involving contacting an inanimate object with thefibers. Examples of such inanimate objects include those with sharpand/or dull edges. Such processes also involve, for example, cutting,kneading, pounding, impaling, and the like, and combinations thereof.

Nonlimiting examples of chemical modifications include conventionalchemical fiber processes such as crosslinking and/or precipitation ofcomplexes thereon. Other examples of suitable modifications of fibersinclude those found in U.S. Pat. Nos. 6,592,717, 6,592,712, 6,582,557,6,579,415, 6,579,414, 6,506,282, 6,471,824, 6,361,651, 6,146,494,H1,704, 5,731,080, 5,698,688, 5,698,074, 5,667,637, 5,662,773,5,531,728, 5,443,899, 5,360,420, 5,266,250, 5,209,953, 5,160,789,5,049,235, 4,986,882, 4,496,427, 4,431,481, 4,174,417, 4,166,894,4,075,136, and 4,022,965, the entire contents of each of which arehereby incorporated, independently, by reference.

Some examples of fluff, which are not intended to be limiting, includethose commercially available RW Supersoft™, Supersoft L™, RW SupersoftPlus™, GT Supersoft Plus™, RW Fluff LITE™, RW Fluff 110™, RW Fluff 150™,RW Fluff 160™, GP 4881™, GT Pulp™, RW SSP™, GP 4825™, alone, or in anycombination.

As discussed herein, if desired, additives such as pH adjusting agent,whitener, colorant, pigment, optical brightening agent, wetting agent,binder, bleaching agent, trivalent cationic metal, alum, other additive,or a combination thereof may be utilized. Such compounds are known inthe art and otherwise commercially available. Given the teachingsherein, one of ordinary skill in the fluff pulp and fluff pulppapermaking arts would be able to select and use them as appropriate. Ifpresent, the amount of additive is not particularly limited. In oneembodiment, the additive may be present in amounts ranging from about0.005 to about 50 weight percent based on the weight of the fluff pulpsheet. This range includes all values and subranges therebetween,including about 0.005, 0.006, 0.007, 0.008, 0.009, 0.01, 0.02, 0.03,0.04, 0.05, 0.06, 0.07, 0.08, 0.09, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30, 35, 40, 45, and50 weight percent, or any combination thereof, based on the weight ofthe finished fluff pulp sheet.

One or more optical brightening agents may be optionally present.Typically, the optical brightening agents are fluorescent dyes orpigments that absorb ultraviolet radiation and reemit it at a higherwavelengths in the visible spectrum (blue), thereby effecting a white,bright appearance to the paper sheet when added to the stock furnish,but any optical brightening agent may be used. Examples of opticalbrighteners include, but are not limited to azoles, biphenyls,coumarins, furans, stilbenes, ionic brighteners, including anionic,cationic, and anionic (neutral) compounds, such as the Eccobrite™ andEccowhite™ compounds available from Eastern Color & Chemical Co.(Providence, R.I.); naphthalimides; pyrazenes; substituted (e.g.,sulfonated) stilbenes, such as the Leucophor™ range of opticalbrighteners available from the Clariant Corporation (Muttenz,Switzerland), and Tinopar™ from Ciba Specialty Chemicals (Basel,Switzerland); salts of such compounds including but not limited toalkali metal salts, alkaline earth metal salts, transition metal salts,organic salts and ammonium salts of such brightening agents; andcombinations of one or more of the foregoing agents.

Examples of optional fillers include, but are not limited to, clay,calcium carbonate, calcium sulfate hemihydrate, and calcium sulfatedehydrate, chalk, GCC, PCC, and the like.

Examples of optional binders include, but are not limited to, polyvinylalcohol, Amres (a Kymene type), Bayer Parez, polychloride emulsion,modified starch such as hydroxyethyl starch, starch, polyacrylamide,modified polyacrylamide, polyol, polyol carbonyl adduct,ethanedial/polyol condensate, polyamide, epichlorohydrin, glyoxal,glyoxal urea, ethanedial, aliphatic polyisocyanate, isocyanate, 1,6hexamethylene diisocyanate, diisocyanate, polyisocyanate, polyester,polyester resin, polyacrylate, polyacrylate resin, acrylate, andmethacrylate. Other optional substances include, but are not limited tosilicas such as colloids and/or sols. Examples of silicas include, butare not limited to, sodium silicate and/or borosilicates.

The composition may optionally and additionally include one or morepigments. Nonlimiting examples of pigments include calcium carbonate,kaolin clay, calcined clay, aluminum trihydrate, titanium dioxide, talc,plastic pigment, ground calcium carbonate, precipitated calciumcarbonate, amorphous silica, modified calcium carbonate, modifiedcalcined clay, aluminum silicate, zeolite, aluminum oxide, colloidalsilica, colloidal alumina slurry, modified calcium carbonate, modifiedground calcium carbonate, modified precipitated calcium carbonate, or amixture thereof.

In one embodiment, the modified calcium carbonate is modified groundcalcium carbonate, modified precipitated calcium carbonate, or a mixturethereof. Here, the term, “modified” is sometimes referred to as“structured”. These types of pigments are known to those skilled in thepapermaking art.

The fluff pulp fibers may be formed into a single or multi-ply web on apapermaking machine such as a Fourdrinier machine or any other suitablepapermaking machine known in the art. The basic methodologies involvedin making fluff pulp sheets on various papermaking machineconfigurations are well known to those of ordinary skill in the art andaccordingly will not be described in detail herein. In one embodiment,the fluff pulp mixture or fluff pulp fibers may have the form of arelatively low consistency aqueous slurry of the pulp fibers optionallytogether with one or more additives. In one embodiment, the fluff pulpmixture or fluff pulp fibers slurry is ejected from a head box onto atable, e.g., a porous endless moving forming sheet or wire, where theliquid, e.g., water, is gradually drained through small openings in thewire, optionally with the aid of one or more suction boxes, until a matof pulp fibers and optionally the other materials is formed on the wire.The debonder surfactant may be applied to the web at any point along thetable, for example, by spraying from a formation shower. In oneembodiment, the still-wet web is transferred from the wire to a wetpress where more fiber-to-fiber consolidation occurs and the moisture isfurther decreased. In one embodiment, the web is then passed to a dryersection to remove a portion of, most of, or substantially all of theretained moisture and further consolidate the fibers in the web. Afterdrying, the dried web or fluff pulp sheet may be further treated withone or more of the same or different debonder surfactant, or anycombination thereof with a formation shower, spray boom, or the like.

The precise location where the respective compositions are applied orcontacted may depend on the specific equipment involved, the exactprocess conditions being used and the like. These are easily determinedgiven the teachings herein combined with the knowledge of one ofordinary skill in the papermaking art.

EXAMPLES

The claimed subject matter may be described in further detail withreference to the following examples. The examples are intended to beillustrative, but the claimed subject matter is not considered as beinglimited to the materials, conditions, or process parameters set forth inthe examples. All parts and percentages are by unit weight unlessotherwise indicated.

The various tests for which results are described herein are providedbelow:

Fluff Pulp Fiberization Test Procedure or “Johnson Nit” Test:

1. 5.00 g of defibered pulp is placed into the Johnson Nit Counter.

2. Air pressure is set to 100 psi and the test time is set to 600seconds.

3. At the end of the test the amount retained on the No. 16 screen isweighed and recorded.

4. Then the amount retained on the No. 30 screen is weighed andrecorded.

5. The difference between the initial amount and amount retained on thetwo screens is recorded as the amount passing the No. 30 screen.

Multi-Dose Acquisition Test Procedure:

1. A 5″×12″ fluff pulp sample was compressed to a density of 0.154gms/cm3 using a Beloit Wheeler calendar roll.

2. A sheet of MTS produced coverstock was placed on top of thecompressed sample.

3. A 1″ diameter dosing tube weighing 1000 g was centered on top of thesample.

4. 30 mls of 0.9% saline solution was dosed at a flow rate of 7 mls/sec.

5. Timing began once the dosage started and ended when all of the salinesolution was absorbed and the absorption time was recorded.

6. After 300 seconds after the first dose was absorbed a second dose ofsaline solution was applied and the timing procedure was repeated andthe absorption time recorded.

7. 300 seconds after the second dose was absorbed a third dose wasapplied and the timing procedure was repeated and the absorption timerecorded.

Kamas Mill—Fluff Pulp Shredding:

The Kamas hammermill is a simulation of commercial equipmentmanufactured and supplied by Kamas Industri AB for use in the productionof fluff pulp products. Like the commercial equipment it has variablerotor speed, variable pulp feed speed and exchangeable screens. Pulpstrips are hand fed into the mill and are defiberized with free swinginghammers until the resultant fluff is sufficiently broken up to passthrough the screen holes.

Fluff Testing Room: Controlled conditions, 72° F. and 55% (+/−5)relative humidity

Apparatus: Kamas Type H 01 Laboratory Defribrator

Sample Preparation: Condition pulp sheets in the testing room for atleast 4 hours. For lab test sheets, trim about ½″ from edges. Cut pulpsheets into strips, 5-10 strips/sample if available, 2 inches wide.Record weights. Clean dust bag if necessary. Ensure that milling chamberis clean and desired screen is properly inserted. Make sure thecollection funnel/screen is securely in place. Set rotor to 3300 rpm,feed to 15 cm/sec and use 10 mm screen unless otherwise specified. Feedpulp strip into mill. The energy will be automatically measured anddisplayed. Make sure weight entry is correct. Collect the shredded pulpin the collection screen receptor below the shredding chamber—maximumcapacity is 4-5 strips. Empty fluff into plastic bag. Mix by hand, thenseal bag and shake vigorously to get a homogenous fluff mix.

4 Screen Fractionation of Shredded Fluff Pulp:

Purpose: To determine the size distribution of fibers in dry shreddedpulp. A moving high velocity air stream disperses shredded pulp in acovered standard testing sieve while individual fibers are removedthrough the wire mesh by an applied vacuum. The amount of fluff retainedon the sieve wire is determined by weight. The fiber is subjected tofractionation through a series of sieves with consecutively increasinghole openings. The fractions are calculated as a percentage of theoriginal whole fluff weight.

Apparatus: Pulp fluff air turbulence generator and separator

USA Standard Testing Sieves: 8″ diameter×2″ height.

-   -   USA Std #200 (75 um hole opening)    -   USA Std #50 (300 um hole opening)    -   USA Std #14 (1400 um hole opening)    -   USA Std #8 (2360 um hole opening

Notes: This test must be conducted in a controlled room, 48% to 52%relative humidity, 70° F. to 72° F.

Procedure: (1) Condition shredded pulp at least 4 hrs in the test room.Mix the fluff in the plastic bag by hand and by vigorously shaking thesealed bag which contains air space, to achieve as uniform adistribution of fiber fractions as possible, i.e., to achieve arepresentative test sample. (2) Take pulp from various areas of the bag,and weigh out 5 grams (+/−0.01 grams). Record weight, and place on atared #200 sieve. Place sieve on the fluff fractionator and cover. Sealthe seam formed by the sieve with the large rubber gasket. This allows amore uniform distribution of the air/vacuum. (3) Set timer for 5 minutesand start the fractionator by turning knob to “auto”. Adjust thecompressed air to 30 psi and the vacuum to 4 inches using the threeholed circular plexiglass adjustment device. (Note: Vacuum/air psi maydrift, check intermittently). The fines will pass through the sieve intothe vacuum. At the end of the set time period, the unit shuts offautomatically. When finished, remove the sieve. Remove the cover andweigh the sieve plus the pulp on the tared balance. Record the weight ofpulp remaining on the #200 sieve. The mass of the fines is thedifference in the mass of the pulp before and after fractionation. (4)Tare the #50 sieve and transfer the pulp from step 3 on to the #50sieve, cover, place on fractionator and seal as in step 2. Set timer for5 minutes. Reset the start by turning the knob to off, then back toauto. Start fractionator and proceed as in step 3 (adjust air and vacuumas needed). Record the weight of the pulp retained on the #50 screen.(5) Tare the #14 sieve and transfer the pulp from the #50 on to the #14sieve, cover, place on fractionator and seal as in step 2. Set timer for5 minutes. Reset the start by turning the knob to off, then back toauto. Start fractionator and proceed as in step 3 (adjust air and vacuumas needed). Record weight of the pulp retained on the #14 screen. (6)Transfer the pulp from the #14 to the #8 screen. Repeat the processabove (5 minutes, 30 psi, vacuum at 4 in.) and record the weight of pulpretained on the #8. Percent passing #200 is reported as Fines. Percentretained on #200 screen, but passing #50 is reported as Good. Percentretained on #50, but passing #14 is reported as Good (Total Good is sumof the two good fractions). Percent retained on #14 screen, but passing#8 screen is reported as Nits (fiber agglomerates). Percent retained on#8 screen is reported as Pieces.

Calculations:

Original Fluff Weight

Weight remaining on #200

Weight remaining on #50

Weight remaining on #14

Weight remaining on #8

$\begin{matrix}{{{Percent}\mspace{14mu}{passing}\mspace{14mu}{\# 200}} = {{\frac{(1) - (2)}{(1)} \times 100} = {\%\mspace{14mu}{Fines}}}} \\{{{Percent}\mspace{14mu}{retained}\mspace{14mu}{on}\mspace{14mu}{\# 200}} = {{\frac{(2) - (3)}{(1)} \times 100} = {\%\mspace{14mu}{Good}}}} \\{{{Percent}\mspace{14mu}{retained}\mspace{14mu}{on}\mspace{14mu}{\# 50}} = {{\frac{(3) - (4)}{(1)} \times 100} = {\%\mspace{14mu}{Good}}}} \\{{{Percent}\mspace{14mu}{retained}\mspace{14mu}{on}\mspace{14mu}{\# 14}} = {{\frac{(4) - (5)}{(1)} \times 100} = {\%\mspace{14mu}{{Nits}\left( {{fiber}\mspace{14mu}{agglomerates}} \right)}}}} \\{{{Percent}\mspace{14mu}{retained}\mspace{14mu}{on}\mspace{14mu}{\# 8}} = {{\frac{(5)}{1} \times 100} = {\%\mspace{14mu}{Pieces}}}}\end{matrix}$

Run a minimum of three tests per sample.

Scan Absorption Test:

Purpose: To determine absorption properties of fluff pulp pads. Themethod is based on the Scandinavian standard SCAN-C 33:80. Fluff volume(bulk), absorption rate and absorption capacity are measured by placinga test pad on the unit, applying a uniform load and allowing the pad toabsorb liquid from below until saturated.

Apparatus: SCAN Absorption Tester consisting of a test piece former,absorption unit and timing device.

Reagents: 0.9% saline (NaCl) solution

Procedure: (1) Prepare saline solution, 0.9% sodium chloride in DI water(e.g., 180 g/20 L) and transfer to saline delivery carboy. (2) Setup:Rinse electrode platen and blot dry with wipe; rinse screen andreservoir to remove residue, dry and replace in tester. Open valve oncarboy and run saline through until it flows into overflow pail. Closevalve. May need to stabilize the instrument by running a few samplesbefore analyzing test samples. (3) Mix fluff by vigorously shakinginflated sample bag. Weigh out approximately 3.20 g of fluff pulp (takeseveral small portions throughout the bag to get a representativesample). (4) Tare the forming tube (the plexiglass cylindrical mold with50 mm base screen) and place securely on pad former (make sure it'sfirmly seated on gasket). Turn on vacuum and carefully feed the pulpinto the former in small amounts, allowing fibers to separate as much aspossible. Avoid feeding in clumps of pulp. (5) After pad has been formedturn off vacuum and remove mold/screen assembly. Place tared assemblywith pad on balance and remove excess pulp to give a final weight of3.00 g+/−0.01. Arrange pulp as needed to give uniform thickness. Fiberssometimes build up on one side in tube, especially if high in nits.Remove from this area first to get the 3.00 g, then rearrange as needed,carefully lifting mat/fibers to the thinner area. Gently tamp down themoved fibers to give a uniform thickness. Prepare 6-8 pads per sample.(6) Setup computer: Turn computer on. Enter ID and sample wt (i.e., 3.00g). (7) Pre-wet the SCAN tester sample basket and use wipe to removeexcess. Lower the electrode platen and click “Zero” on the computer tozero height sensor. Raise and latch the electrode platen. (8) Removebottom screen from forming tube. Place plexi tube on the SCAN wirebasket; gently lower the electrode platen (with the load on top ofshaft) onto the pad, carefully raise the mold (hold in place), click“Start” on computer to start the timer on computer screen, then swingholder over and rest the tube on it. Avoid touching the wires and shaftwith the tube. Watch the screen and start the saline flow at about 18-20seconds. When prompted (at 30 sec), raise the reservoir in one evenmotion (hold in place) and immediately start manual timer. Watch the padand stop manual timer as soon as liquid has wicked up. When prompted onthe computer screen, carefully lower the reservoir, close the salinevalve and allow pad to drain. When prompted “test over”, raise theelectrode platen up through the former tube. If pad sticks to theplaten, gently tap with edge of tube to release pad onto the basket.Latch the electrode platen, remove forming tube and carefully transferpad to a balance. Record wet weight. Enter wet pad weight in instrumentcomputer. Record the dry height (caliper, mm), specific volume (cc/g),absorption time (sec), and absorption capacity as displayed, and themanual time wet weight, on spreadsheet. Report absorption time (sec),absorption rate (cm/sec), specific volume (g/cc), and capacity (g/g).Run 6-10 tests per sample. Report averages and SD.

Example 1

In Samples 719-727, A Commercially Available Debonder Surfactant, F60,available from Akzo Nobel, was sprayed onto dried webs comprising fluffpulp fibers in accordance with one or more embodiments of the claimedsubject matter. The moisture content of the dried webs was 6.3%. The LAControl and NB 405 samples are provided for comparison, and arecommercially available untreated and treated fluff pulp sheets,respectively.

TABLE 1 F60 Debonder Surfactant F60 Debonder Targeted Dose SurfactantFiberization lbs F60/ton of Solution energy Sample dry fiberConcentration % kJ/kg Mullen PSI 719 2.5 7.5 91 125 720 3 7.5 84 122 7213.5 7.5 77 103 722 2.5 8.5 70 122 723 3 8.5 86 136 724 3.5 8.5 71 122725 2.5 9.5 77 133 726 3 9.5 90 133 727 3.5 9.5 70 128 LA 0 0 135 168Control NB 405 NA NA 86 83

The spray-on application of F60 produces a fluff pulp sheet with afiberization energy equal to a fully treated fluff pulp (NB 405 asexample), but surprisingly the sheet Mullen doesn't drop to a low level.This enables the sheet to remain processable through the winder at highspeeds without sheet breaks or processing issues. The spray-onapplication occurred on a fully dried sheet in this example, 6.3% MC. Ifdesired, the chemical and sheet can both be heated (˜160° F.) or roomtemperature during application. One advantage of adding the debonder tothe dry fluff sheet (of 100 to 1100 GSM basis weight) is the issue ofconveying a mechanically weak sheet through the paper machine isavoided. Surfactant retention is also improved.

Without wishing to be bound by theory, it is possible that the fact thatthis spray-on application works because some migration or mixing of thechemical occurs during fiberization. Shred quality or fiber singulationis equal to traditional debonder application methods, but processingdifficulties, e.g., sheet breaking, etc., is significantly improved.

F60 will not retain if added to the stock before the headbox. Withoutwishing to be bound by theory, it is possible that the chemistryrequired for a surfactant that helps to reduce the energy to separatethe fibers during fiberization, but doesn't induce large reduction inabsorption rate of fluff core, must be only slightly cationic. Thehighly polar surfactants retain well on the pulp fiber but they tend tocreate a fluff core with significantly reduce absorption properties(Re-wet and rate of absorption).

From the results shown in the tables and graphically illustrated in theFigures, it is clear that the examples within the scope of oneembodiment of the invention inhere surprising and unexpectedly superiorbenefits when compared to those comparative examples.

As used throughout, ranges are used as a short hand for describing eachand every value that is within the range, including all subrangestherein.

All other references, as well as their cited references, cited hereinare hereby incorporated by reference with respect to relative portionsrelated to the subject matter of the present invention and all of itsembodiments.

Numerous modifications and variations on the present invention arepossible in light of the above teachings. It is, therefore, to beunderstood that within the scope of the accompanying claims, theinvention may be practiced otherwise than as specifically describedherein.

What is claimed is:
 1. A process for making a fluff pulp sheet,comprising: forming a web comprising fluff pulp fibers, and spraying atleast one debonder surfactant to the web prior to a dryer section andafter a headbox of a papermaking machine, to make the fluff pulp sheet;wherein the fluff pulp sheet a fiberization energy of <145 kJ/kg and aMullen of ≥90 psi, and wherein the debonder surfactant is one or moreselected from the group consisting of linear or branched monoalkylamine, linear or branched dialkyl amine, linear or branched tertiaryalkyl amine, linear or branched quaternary alkyl amine, fatty acidamide, fatty acid amide quaternary ammonium salt, dialkyl dimethylquaternary ammonium salt, dialkylimidazolinium quaternary ammonium salt,dialkyl ester quaternary ammonium salt, triethanolamine-ditallow fattyacid, dialkyl amide of fatty acid, dialkyl amide of fatty acid, compoundhaving CAS Registry No. 68155-01-1, compound having CAS Registry No.26316-40-5, and a combination thereof.
 2. The process of claim 1,wherein the forming comprises one or more of contacting a fluff pulpmixture comprising fluff pulp fibers and water with a table in thepapermaking machine, removing at least a portion of water from a fluffpulp mixture comprising fluff pulp fibers and water with a suction boxunder a table in a papermaking machine, at least partially drying afluff pulp mixture comprising fluff pulp fibers and water in a flotationdryer, heating a fluff pulp mixture comprising fluff pulp fibers andwater, heating the debonder surfactant, or a combination thereof.
 3. Theprocess of claim 1, wherein the spraying is carried out using one ormore formation showers over a table in the papermaking machine.
 4. Theprocess of claim 1, further comprising drying the web in a dryer, toform a dried web.
 5. The process of claim 1, wherein the web has amoisture content of about 6.3%.
 6. The process of claim 1, wherein theweb has a basis weight of 100 to 1100 gsm.
 7. The process of claim 1,wherein the web further comprises water and optionally one or moresecond debonder surfactant, pH adjusting agent, whitener, colorant,pigment, optical brightening agent, wetting agent, binder, bleachingagent, trivalent cationic metal, alum, other additive, or a combinationthereof.
 8. The process of claim 1, wherein the web comprises a solidscontent of >1% by weight.
 9. The process of claim 1, wherein thedebonder surfactant is neat, in combination with one or more seconddebonder surfactant, in solution, or combination thereof.
 10. Theprocess of claim 1, wherein the debonder surfactant is in the form of acomposition further comprising water and optionally one or more pHadjusting agent, whitener, colorant, pigment, optical brightening agent,wetting agent, binder, bleaching agent, trivalent cationic metal, alum,other additive, or a combination thereof.
 11. The process of claim 1,further comprising fiberizing or shredding the fluff pulp sheet.
 12. Theprocess of claim 11, wherein the fiberizing or shredding are carried outin a hammermill.
 13. The process of claim 1, further comprisingincorporating the fluff pulp sheet into one or more of an adsorbentproduct, paper product, personal care product, medical product,insulating product, construction product, structural material, cement,food product, veterinary product, packaging product, diaper, tampon,sanitary napkin, gauze, bandage, fire retardant or a combinationthereof.
 14. A fluff pulp sheet, comprising: a web comprising fluff pulpfibers; at least one debonder surfactant selected from the groupconsisting of linear or branched monoalkyl amine, linear or brancheddialkyl amine, linear or branched tertiary alkyl amine, linear orbranched quaternary alkyl amine, fatty acid amide, fatty acid amidequaternary ammonium salt, dialkyl dimethyl quaternary ammonium salt,dialkylimidazolinium quaternary ammonium salt, dialkyl ester quaternaryammonium salt, triethanolamine-ditallow fatty acid, dialkyl amide offatty acid, dialkyl amide of fatty acid, compound having CAS RegistryNo. 68155-01-1, compound having CAS Registry No. 26316-40-5, and acombination thereof; a fiberization energy of <145 kJ/kg; and a Mullenof ≥90 psi.
 15. The sheet of claim 14, further comprising a SCAN-C 33:80adsorption time of <4.0 s.
 16. The sheet of claim 14, further comprisingon screen fractionation a % Good of ≥50%.
 17. The sheet of claim 14,further comprising on screen fractionation a % Fines of ≤40%.
 18. Thesheet of claim 14, further comprising on screen fractionation a % Piecesof ≤30%.
 19. The sheet of claim 14, wherein the debonder surfactant ispresent in an amount of ≥1 lb per ton of the fluff pulp fibers.
 20. Thesheet of claim 14, further comprising a moisture content of about 6.3%.21. The sheet of claim 14, further comprising a density of 0.5 to 0.75g/cc.
 22. The sheet of claim 14, further comprising a caliper of 40 to70 mm.
 23. The sheet of claim 14, further comprising a finished basisweight of 100-1100 gsm.
 24. An adsorbent product, paper product,personal care product, medical product, insulating product, constructionproduct, structural material, cement, food product, veterinary product,packaging product, diaper, tampon, sanitary napkin, gauze, bandage, fireretardant, or a combination thereof, comprising the sheet of claim 14.